EP2329147B1 - Pumping device - Google Patents
Pumping device Download PDFInfo
- Publication number
- EP2329147B1 EP2329147B1 EP09777900.3A EP09777900A EP2329147B1 EP 2329147 B1 EP2329147 B1 EP 2329147B1 EP 09777900 A EP09777900 A EP 09777900A EP 2329147 B1 EP2329147 B1 EP 2329147B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pulsator
- pressure
- pump device
- line
- working space
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000005086 pumping Methods 0.000 title description 5
- 238000013022 venting Methods 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 19
- 238000013461 design Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 238000010276 construction Methods 0.000 claims description 4
- 210000004379 membrane Anatomy 0.000 description 52
- 239000012528 membrane Substances 0.000 description 51
- 239000002245 particle Substances 0.000 description 29
- 239000007787 solid Substances 0.000 description 25
- 238000000034 method Methods 0.000 description 17
- 230000008569 process Effects 0.000 description 17
- 230000008901 benefit Effects 0.000 description 14
- 238000010586 diagram Methods 0.000 description 9
- 238000009423 ventilation Methods 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- 239000012530 fluid Substances 0.000 description 5
- 238000007639 printing Methods 0.000 description 4
- 239000002028 Biomass Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000002551 biofuel Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
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- 238000013508 migration Methods 0.000 description 1
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- 230000003313 weakening effect Effects 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
- F04B53/06—Venting
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B43/00—Machines, pumps, or pumping installations having flexible working members
- F04B43/02—Machines, pumps, or pumping installations having flexible working members having plate-like flexible members, e.g. diaphragms
- F04B43/06—Pumps having fluid drive
- F04B43/067—Pumps having fluid drive the fluid being actuated directly by a piston
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
- F04B53/08—Cooling; Heating; Preventing freezing
Definitions
- the invention relates to a pump device with a pulsator as a drive element for a main pump head, which is located in a delivery line and whose working space is provided with a suction-side check valve and a pressure-side check valve, according to the preamble of claim 1.
- a membrane pulsator is to be understood such that it corresponds to a piston membrane pump, which does not necessarily have check valves on the suction and pressure side, but otherwise generally has all the features of a piston membrane pump.
- a piston diaphragm pump to be a piston pump coupled to a diaphragm, the deflection of the piston being transmitted to the diaphragm via a hydraulic coupling.
- Membrane pulsators can in particular, like piston diaphragm pumps, have a preferably diaphragm-controlled refill and / or venting device for the hydraulic fluid, such as that from the EP 0 085 725 A1 is known.
- the invention relates to a pump device with a pulsator, in particular a membrane pulsator, as a drive element for a main pump head, which is located in a delivery line and whose working space is provided with a suction-side check valve and a pressure-side check valve.
- the work area of the pulsator is directly connected to the work area of the main pump head via a pendulum line filled with the pumped medium in such a way that the pulsator oscillates the pumped medium from the delivery line into the work area of the main pump head or presses it out of the work area.
- the pump device according to the invention is particularly well suited for conveying suspensions, such as mixtures of biomass and supercritical water, and in particular for high pressures and temperatures.
- Pumps of this type are out EP 0919724 B1 .
- a main pump head located in the delivery line is driven by another pump head, which is referred to as a pulsator.
- Such a pump device is also referred to as a "remote head” pump.
- Pump devices of this type are typically used for pumping liquids with a high solids content and high temperatures.
- the known pumps cannot readily be used with particularly aggressive delivery media, such as supercritical aqueous solutions, in particular when processes with a very high throughput are present at high temperatures and high pressures.
- FIG. 2004/062662 A1 Another type of pump device, namely a diaphragm metering pump for metering a shower gas, is in the US 2004/062662 A1 described.
- This pump has a pump head with a product chamber with an inlet end with an inlet valve and an outlet end with an outlet valve.
- a sliding membrane element defines a boundary of the product chamber. The membrane element can be moved back and forth to cause pump displacements.
- An exhaust side is located downstream of the exhaust valve.
- a passage is arranged in fluid communication between the delivery side and the product chamber.
- a valve is located in the passage. The valve is opened intermittently to allow the liquid to flow back into the product chamber in an amount that can be used to remove the gas from the product chamber to avoid loss of ventilation.
- the invention has for its object to provide a pump device of the type mentioned, which can be used for pumping aggressive fluids at high temperature, and yet works at low cost with high reliability, which is why in particular an entry of solid particles in the pulsator can be avoided should.
- a pump device with a pulsator as a drive element for a main pump head which is located in a delivery line and whose work space is provided with a suction-side check valve and a pressure-side check valve, is specified, the work space of the pulsator being connected to the work space of the main pump head via a pendulum line filled with the conveyed medium is connected in such a way that the pulsator sucks conveying medium from the delivery line into the working chamber of the main pump head in an oscillating manner or presses it out of the working chamber, a vent valve being provided for venting the working chamber of the pulsator, the vent valve being a time-controlled valve and / or a pressure-controlled one Double seat valve and a device for introducing a liquid into the working space of the pulsator and / or the pendulum line is provided.
- a time-controlled valve and / or a pressure-controlled double-seat valve has the advantage that the time in which the valve is open for venting can be kept very short, as a result of which undesirable secondary flows can be avoided, which increase the entry of solid particles into the pulsator could result.
- the introduction of liquid into the working area of the pulsator or the refilling of pumped medium into the working area to compensate for losses, for example by venting the working area, has the advantage that liquid balance does not have to take place from the driven main pump head and thus no solid particles from the main pump head to be transported to the pulsator.
- the liquid is preferably water and / or delivery medium and / or another suitable liquid.
- the device for introducing a liquid into the work space of the pulsator and / or the pendulum line preferably comprises a time and / or pressure-controlled refill valve and / or a refill reservoir.
- the time and / or pressure-controlled refill valve or vent valve is preferably time and / or pressure controlled such that after a start-up phase of the process the refill valve or vent valve is closed and / or the upper limit value for closing the time and / or pressure-controlled refill valve or vent valve is increased after a start-up phase of the process and / or after a start-up phase of the process the lower limit value for closing the time and / or pressure-controlled refill valve or vent valve is lowered.
- the pressure which is applied to the refill reservoir preferably corresponds essentially to the pressure in the working space of the pulsator.
- the refill valve between the work space and the refill reservoir is preferably a time and / or pressure-controlled valve.
- the working space of the pulsator is preferably connected to the suction side of the delivery line via the and / or a further vent valve.
- the suction side of the delivery line for automatic venting is advantageously arranged above the venting valve.
- the working space of the pulsator is preferably connected to the pressure side of the delivery line via the and / or a further vent valve.
- the vent valve is preferably positively controlled in connection with a return pump, in particular timed.
- the working area of the pulsator is preferably connected via the and / or a further vent valve to a refill reservoir to compensate for leakage shrinkage in the working area of the pulsator and / or the pendulum line.
- the working space of the pulsator is preferably connected via the and / or a further vent valve to a collecting container for collecting and for possibly returning the conveyed medium emerging during the venting.
- the valve is preferably time and / or pressure controlled in such a way that it is closed at least above a certain pressure.
- the pulsator generates a continuously alternating pressure in the work area with a pressure phase and a suction phase.
- at least a certain pressure in the work area should not be vented in order to prevent a pressure drop in the work area, albeit a small one, and thus a reduction in the flow from the pendulum line .
- the valve is preferably time and / or pressure controlled such that it is closed at least below a certain pressure.
- venting below a certain pressure in the pulsator's working space is preferably avoided, because the, albeit small, pressure drop would result in greater suction power and thus a stronger flow into the pendulum line, which could suck more solid particles into the pendulum line. Therefore, the valve is preferably closed at least below a certain pressure in the work area.
- the venting preferably takes place only in the time ranges between the suction and the pressure phase, where there is essentially little or no flow of the delivery fluid into the pendulum line. This can prevent the flow of solid particles into the pendulum line.
- the pump device preferably has a refill reservoir for refilling the conveyed medium, to which a pressure is applied which essentially corresponds to the system pressure.
- the pendulum line is preferably provided with cooling.
- the pulsator is preferably arranged above the main pump head. Additionally or alternatively, the pendulum line is preferably aligned falling from the pulsator to the main pump head. Such embodiments of the invention have the advantage that gravity additionally counteracts the entry of solid particles through the pendulum line into the pulsator.
- the pendulum line is preferably provided with a depression as a receiving space for solid particles in the conveying medium.
- the working space of the pulsator is preferably at least temporarily acted upon by a compensating medium to compensate for leakage shrinkage.
- the pendulum line is preferably divided into at least one section into at least two parallel sections.
- the pendulum line is preferably also divided over its entire course, i.e. that, for example, two or more parallel pendulum lines are provided.
- the volume of the parallel sections of the pendulum line or the volume of the parallel pendulum lines is preferably at least as large as or preferably larger than the stroke volume of the pulsator.
- Control valves are preferably provided for at least partially opening and closing the sections of the pendulum line or the parallel pendulum lines.
- a sensor system is preferably provided in order to synchronize the timing of the control valves with the respective phase position of the pulsator membrane.
- a sensor and / or switch is provided which switches the control valve in at least one end position of the membrane of the pulsator.
- a sensor and / or switch is provided for the other membrane system in order to switch the control valve.
- the control valves are also put into a closed position or partially closed position only during part of the pressure phase. It would also be conceivable to at least partially close different control valves in succession during a printing phase.
- the pendulum line is preferably divided in the area in front of the main pump head into a plurality of lines connected in parallel, preferably two lines connected in parallel, which are at least partially and preferably completely at least partially closable by a time and / or pressure-controlled valve.
- the time and / or pressure control is preferably set in such a way that all lines are open for as long as possible during the suction phase, so that the flow adjusts to the different ones in parallel Lines distributed, while in the pressure phases alternately a partial line with the full pressure and thus a much higher flow rate. As a result, the entry of solid particles into the pendulum line should be avoided.
- the main pump head preferably has at least two suction-side check valves connected in parallel.
- This embodiment of the invention has the advantage that a higher flow velocity is generated in the line section between the outlets of the two suction-side check valves during the pressure phase, so that the risk of solid particles entering the pendulum line from the suction side downstream of the flow direction during the pressure phase Check valve is reduced.
- the cross section of the line receiving the downstream suction-side check valve in relation to the flow direction during the pressure phase is preferably larger than the cross section of the line receiving the other suction-side check valve.
- the cross sections of the two lines could also be the same size or more than two lines and a corresponding number of check valves on the suction side could be provided. It would also be conceivable to have a larger cross section of the line receiving upstream suction-side check valve in relation to the direction of flow during the pressure phase, which still offers an advantage, albeit a smaller one, than the designs with only one suction-side check valve.
- a separating piston is preferably arranged in the pendulum line.
- the above-mentioned embodiments of the pump device according to the invention are preferably designed with a double-acting pulsator and two pump circuits controlled in opposite directions.
- the pulsator is preferably designed as a double-acting pulsator, one side of which is designed as a drive element for the main pump head, and the other side of which is acted upon by a pressure which essentially corresponds to the system pressure.
- Such embodiments of the invention with a double-acting pulsator for driving two mutually controlled pump circuits are preferred, since this enables uniform delivery.
- the pulsator can be driven at high suction pressures of, for example, 250 bar with a drive designed for significantly lower pressures, for example if a double-acting piston is used, which only the differential pressure between the pressure during the pressure phase in one half of the pulsator and the pressure during the Must overcome suction phase in the other half of the pulsator.
- This advantage also applies to double-acting pulsators for driving only one pump circuit when pressure is applied to the other side of the pulsator, which does not drive the pump circuit.
- the refill reservoir is pressurized with a pressure that approximately corresponds to the system pressure, so that the drive also takes place during the refill process, which is valve-controlled when the membrane is its rear mechanical system achieved, is not exposed to a higher pressure than the differential pressure between the suction and pressure phases and therefore does not have to be dimensioned larger, and the membrane is not destroyed at the flow channels of its rear mechanical system.
- a membrane system-controlled refill and / or venting device for hydraulic fluid can be provided in the pulsator, such as that from the EP 0 085 725 A1 is known.
- Compensating medium for compensating for leakage shrinkage is preferably present in the diaphragm control chamber in a refill reservoir which is connected to the diaphragm control chamber via a valve, the refill reservoir being pressurized to a pressure which is higher than atmospheric pressure.
- This embodiment of the invention has the advantage that the pulsator can be driven by a drive (for example hydraulically, mechanically and / or pneumatically, for example a piston drive), the power of which only has to overcome the pressure difference between the suction and the pressure side.
- a drive for example hydraulically, mechanically and / or pneumatically, for example a piston drive
- an impact on the drive, for example the piston can be prevented by pressurizing the refill reservoir to compensate for leakage in the membrane control chamber.
- This pressure in the refill reservoir can advantageously correspond approximately to the system pressure.
- a pressure control which is adapted to the system pressure by means of a control loop is provided in the refill reservoir, as is the case, for example, in EP 1 898 093 A1 is described.
- the pulsator is preferably constructed in the form of a membrane or tubular membrane.
- the pulsator is preferably designed in a piston or plunger construction.
- a basic idea of the invention is therefore that the pulsator acts on a main pump head, which is basically designed like a piston pump head, but without the need for a piston.
- a standard component that is suitable for high temperatures and pressures can be used as the pump head, which, combined with a standard membrane pulsator, is an inexpensive alternative to the known solutions, while maintaining the principle of a "remote head” pump.
- the wear is further reduced by the fact that any particles present in the pumped medium do not come into contact with the working area of the pulsator, since the liquid in the pendulum line is only moved back and forth in the circumference of the pump stroke and mixes only slightly with freshly drawn-in liquid.
- the pulsator can be constructed in membrane or tubular membrane construction as well as in piston or plunger construction. If the pulsator is a membrane pulsator, particles do not get to the membrane. Since high temperatures in the pumped medium also decrease in the course of the pendulum line, membrane pulsators with inexpensive plastic membranes, for example made of PTFE, can also be used in the delivery line at high pressures and high temperatures. Pump devices according to the invention are therefore particularly well suited for conveying biomass in the production of biofuel.
- Another advantage is that, due to the ventilation, gases from the pumped medium or air inclusions cannot accumulate in the pump room of the pulsator, but are returned to the process.
- the entry into the suction-side delivery line is preferably above the ventilation valve, so that the gases exit the working area automatically.
- there may be a forced ventilation for example with a time and / or pressure controlled valve.
- the pendulum line is provided with cooling.
- the pendulum line is aligned to fall from the membrane pulsator to the main pump head. The particles thus remain in the area of the main pump head and are returned to the delivery line.
- the pendulum line can be provided with a depression as a receiving space for solid particles in the conveying medium.
- An area is therefore provided in the pendulum line which lies below the working space of the membrane pulsator, so that the particles collect there due to gravity and do not get into the working space of the pulsator.
- the working space of the pulsator is acted upon by a compensating medium to compensate for leakage shrinkage, so that flow through the pendulum line and migration of solid particles to the pulsator are prevented.
- a further advantageous embodiment of the invention consists in arranging a separating piston in the pendulum line. This measure separates the part of the pendulum line assigned to the pulsator from the part assigned to the main pump head.
- a low drive power is achieved in that there is a double-acting pulsator and two counter-driven pump circuits, which is particularly advantageous when used in recirculation processes with high suction pressures.
- a pump device 1 has a membrane pulsator 10 serving as a pulsator, a main pump head 11 and a pendulum line 12.
- the main pump head 11 has an inlet 13 and an outlet 14 for installation in a delivery line, the pressure side of which is designated 5 and the suction side of which is 15.
- the direction of conveyance is marked with arrow 6.
- the main pump head 11 corresponds to a pump head of a piston pump. However, it has no piston.
- the membrane pulsator 10 is provided with a connection 7 for the pendulum line 12. Furthermore, a connection 8 for ventilation with a ventilation valve 9 ( Fig. 2 ) and a connection 4 for a refill reservoir 30 ( Fig. 2 ) available.
- a ventilation valve 9 Fig. 2
- a refill reservoir 30 Fig. 2
- the pendulum line 12 is filled with liquid 21. It leads via a control input 22 of the main pump head 11 to the working space 20 of the diaphragm pulsator 10.
- the pendulum line 12 is provided with a cooling system, which is formed by a cooling jacket 23 charged with coolant becomes. In this way, a temperature reduction of, for example, approximately 360 ° C. at the main pump head 11, as is typically the case with the bio mass to be conveyed in the production of bio-fuels, to approximately 100 ° C. on the membrane pulsator 10.
- the pendulum line 12 contains the conveying liquid 21, which may also have solid particles 24, a section 25 is present in the pendulum line 12, which drops from the membrane pulsator 10 to the main pump head 11 and which opens directly into the working space 18 of the main pump head 11. At its lowest point, the pendulum line 12 is thus at the level of the working space 18 of the main pump head 11. The solid particles 24 remain due to gravity in the working space 18 of the main pump head 11 and do not get into the working space 20 of the membrane pulsator 10. Rather, they become the pressure-side delivery line 5 fed.
- the membrane pulsator 10 has a membrane 26 which is controlled hydraulically via a membrane control chamber 27. PTFE is preferably suitable as the membrane material.
- the membrane control chamber 27 is acted upon by a piston 28 which is mechanically actuated, for example by a motor 29 ( Fig. 2 ), and / or is driven hydraulically and / or pneumatically, for example by alternately pressurizing the chambers next to the disk 281.
- a refill reservoir 30 filled with a compensating medium which is controlled by a controlled valve 31 ( Fig. 2 ) Emits compensation medium into the working space 20 of the membrane pulsator 10.
- the feed is in Fig. 2 designated with 4.
- FIG. 2 The configuration shown has a double-acting pulsator with two pump devices as shown in Fig. 1 are illustrated on.
- the pump devices are connected in parallel in two oppositely controlled branches A, B.
- a pumping process is described using a branch.
- the piston 28 In an initial state, the piston 28 is moved into the membrane control chamber 27 and the membrane 26 is bulged into the working space 20 of the membrane pulsator 10.
- the pendulum line 12 and the working space 18 of the main pump head 11 are completely filled with liquid.
- the suction-side check valve 16 and the pressure-side check valve 17 are closed.
- each main pump head 11 can be controlled in the same or opposite direction with a single-acting pulsator.
- a section of a pendulum line 12 ' is illustrated as a detail of a second exemplary embodiment.
- a separating piston 32 which is mounted to be longitudinally displaceable according to the double arrow 35 is arranged in the pendulum line 12'.
- Possibly existing solid particles 24 thereby remain in an area 33 on the side of the main pump head 11 and cannot reach an area 34 on the side of the membrane pulsator.
- Fig. 1A shows an embodiment with a double-acting pulsator.
- Fig. 1A corresponds essentially to that in Fig. 1 shown embodiment, wherein the pump device of Fig. 1 basically exists twice and is driven by a common piston 28.
- the double-acting pulsator is in Fig. 1A shown extremely simplified, ie without drive and without hydraulic reservoirs and their pressurized refill valves.
- the double-acting piston 28 describes an end position (the membrane 26 is bulged on the right, ie the pressure stroke or the pressure phase is complete; the membrane 26 is flattened on the left, ie the suction stroke or the suction phase is complete).
- Fig. 2 shows an embodiment with ventilation in the suction line 15.
- the refill takes place from a pressure accumulator 30 (with gas cushion) in a time-controlled or pressure-controlled manner during the pressure stroke of the pulsator.
- the circuit symbol used for the valve 31 describes a controlled check valve in which the closing is prevented when actuated.
- the pressure in the refill reservoir 30 must be greater than the system pressure.
- the refill volume flow must be greater than / equal to the leakage flow of the venting process. A subsequent regulation of the storage pressure depending on the changing system pressure is recommended. If necessary, manual control is also possible.
- Fig. 4 shows an embodiment with ventilation in the pressure line 5.
- the refill takes place from a pressure accumulator 30 (with gas cushion) time or pressure controlled during the suction stroke of the pulsator.
- the circuit symbol used for the valve 31 describes a controlled check valve, in which the opening is prevented when actuated.
- the pressure in the refill reservoir 30 must be greater than the suction pressure.
- the refill volume flow must be greater than / equal to the leakage flow of the venting process. A subsequent regulation of the storage pressure depending on the changing suction pressure is recommended. If necessary, manual control is also possible.
- Fig. 5 shows an embodiment with a vent into the refill reservoir 30.
- the refill takes place from a pressure accumulator 30 (with gas cushion) in a time-controlled manner.
- the symbol for the refill valve 31 shows no specific function.
- Fig. 6 shows an embodiment with ventilation in any storage or collection container 36.
- the refill is carried out from a pressure accumulator 30 (with gas cushion) in a time-controlled manner.
- the symbol for the refill valve 31 shows no specific function.
- Fig. 7 shows an embodiment of the invention of a pump device with a single-acting pulsator.
- the venting or refilling can, for example, according to the above-mentioned embodiments of the invention Fig. 2 . Fig. 4 . Fig. 5 or Fig. 6 respectively.
- the vent in the pressure line 5 is shown as an example of one of the possible variants.
- a double-acting pulsator could also be used, the unused side of which is subjected to a pressure which corresponds approximately to the system pressure, for example by means of a pressure accumulator.
- the advantages of a pressurized refill medium for refilling into the diaphragm control chamber could thus be exploited.
- the pressurization of the unused side of the double-acting pulsator has the advantage that a smaller-sized drive can be used if high pressures of, for example, 250 bar have to be overcome by the pump head driven by the pulsator.
- Fig. 8 shows a possible design of the main pump head 11 pump devices according to the invention.
- two check valves 16, 161 on the suction side are provided, which can also have a different size.
- This embodiment has the advantage that a higher flow velocity is generated in the line section between the two suction-side check valves during the pressure stroke of the pulsator.
- the pendulum line 12 has a gradient towards the suction-side check valves 161, 16. During suction, the suction flow is distributed according to the Cross-sectional conditions on the suction-side check valves 161 and 16. As a result of this during suction, a lower flow takes place in the pendulum line section between these two suction-side check valves than it would be if the entire suction quantity were only sucked in through the suction-side check valve 16.
- This flow could ensure that the deposits from the main flow tend to be pumped back again and again.
- Fig. 9 shows a possible design of the pendulum line 12 pump devices according to the invention.
- the pendulum line is divided into at least one section into at least two subsections 121, 122, which are used for suction at the same time in the suction phases with the help of controlled shut-off valves 123, 124 and can be opened and closed alternately in the pressure phases in order to increase the pressure generated by them Outflow velocity in the sections 121, 122 to prevent deposits of the solid particles.
- each section 121, 122 should preferably be at least as large as and preferably larger than the stroke volume of the pulsator. This prevents solid particles from getting behind the control valves in the pressure phase due to the alternate closing.
- each section In a first suction process, each section would initially be filled with particles up to a maximum of half of its volume. The subsequently closed section would possibly keep this state. During the renewed suction process, the partial section would then be completely filled with particles at most, before a complete rinsing out would take place in the printing phase.
- shut-off valves 123, 124 are provided, which should be synchronized exactly with the respective phase position of the pulsator membrane with the aid of sensors.
- Fig. 10 shows a further embodiment of the invention.
- the same parts are provided with the same reference numerals. Reference is made to the description of the above statements.
- the pulsator is shown in somewhat more detail, the drive for the double-acting piston 28 not being shown.
- the course of the hydraulic channels of the double-acting pulsator is shown in more detail.
- the pump device from Fig. 10 has two refill valves 37 of the diaphragm control chamber, which are preferably acted upon by a pressure which approximately corresponds to the system pressure.
- the pressure is made available by a hydraulic pump 38.
- two vent valves 39 are provided for venting the membrane control rooms.
- FIGS. 11 and 12 show schematic PV diagrams that show the time course of the pump pressure over the stroke volume. Starting at the point on the lower left side, you can see very well the steep flank of the pressure rise during the compression phase, the pressure fluctuations due to the valve kinematics, the displacement of the stroke volume (highest pressure at maximum piston speed), as well as the likewise steep decompression phase and the suction phase. (Note: In the present case, the circular process has been shown clockwise in both figures for reasons of illustration.) The dashed line in Fig. 11 shows the required pressure level and a possible time window for a controlled leakage refilling process during the pressure stroke. The average working pressure of the pulsator in the pressure stroke (pD) is slightly higher than the system pressure.
- the dashed line in Fig. 12 shows the required pressure level and a possible time window for a controlled leakage refill process during the suction stroke. When refilling during the suction stroke, it is sufficient if the pressure level is slightly above the suction pressure.
Description
Die Erfindung betrifft eine Pumpenvorrichtung mit einem Pulsator als Antriebselement für einen Hauptpumpenkopf, der in einer Förderleitung liegt und dessen Arbeitsraum mit einem saugseitigen Rückschlagventil und einem druckseitigen Rückschlagventil versehen ist, gemäß dem Oberbegriff von Anspruch 1.The invention relates to a pump device with a pulsator as a drive element for a main pump head, which is located in a delivery line and whose working space is provided with a suction-side check valve and a pressure-side check valve, according to the preamble of
Im Sinne der vorliegenden Offenbarung der Erfindung ist ein Membranpulsator so zu verstehen, dass er einer Kolbenmembranpumpe entspricht, die nicht notwendigerweise saug- und druckseitige Rückschlagventile aufweist, aber ansonsten in der Regel alle Merkmale einer Kolbenmembranpumpe aufweist. Unter einer Kolbenmembranpumpe versteht der Fachmann eine mit einer Membran gekoppelte Kolbenpumpe, wobei die Auslenkung des Kolbens über eine hydraulische Kopplung auf die Membran übertragen wird. Membranpulsatoren können insbesondere ebenso wie Kolbenmembranpumpen eine vorzugsweise membranlagengesteuerte Nachfüll- und/oder Entlüftungsvorrichtung für die Hydraulikflüssigkeit aufweisen, wie sie beispielsweise aus der
Insbesondere betrifft die Erfindung eine Pumpenvorrichtung mit einem Pulsator, insbesondere einem Membranpulsator, als Antriebselement für einen Hauptpumpenkopf, der in einer Förderleitung liegt und dessen Arbeitsraum mit einem saugseitigen Rückschlagventil und einem druckseitigen Rückschlagventil versehen ist. Der Arbeitsraum des Pulsators steht über eine mit Fördermedium gefüllte Pendelleitung unmittelbar mit dem Arbeitsraum des Hauptpumpenkopfes in der Weise in Verbindung, dass der Pulsator oszillierend Fördermedium aus der Förderleitung in den Arbeitsraum des Hauptpumpenkopfes ansaugt oder aus dem Arbeitsraum drückt. Die erfindungsgemäße Pumpenvorrichtung ist besonders gut zum Fördern von Suspensionen, wie zum Beispiel Mischungen aus Biomasse und überkritischem Wasser, und insbesondere für hohe Drücke und Temperaturen geeignet.In particular, the invention relates to a pump device with a pulsator, in particular a membrane pulsator, as a drive element for a main pump head, which is located in a delivery line and whose working space is provided with a suction-side check valve and a pressure-side check valve. The work area of the pulsator is directly connected to the work area of the main pump head via a pendulum line filled with the pumped medium in such a way that the pulsator oscillates the pumped medium from the delivery line into the work area of the main pump head or presses it out of the work area. The pump device according to the invention is particularly well suited for conveying suspensions, such as mixtures of biomass and supercritical water, and in particular for high pressures and temperatures.
Pumpen dieser Art sind aus
Eine andere Art von Pumpenvorrichtung, und zwar eine Membrandosierpumpe zum Dosieren eines Brausegases, ist in der
Der Erfindung liegt die Aufgabe zugrunde, eine Pumpenvorrichtung der eingangs genannten Art anzugeben, die zum Pumpen von aggressiven Fördermedien mit hoher Temperatur eingesetzt werden kann, und die dennoch bei geringen Kosten mit hoher Zuverlässigkeit arbeitet, weshalb insbesondere ein Eintrag von Feststoffteilchen in den Pulsator vermieden werden sollte.The invention has for its object to provide a pump device of the type mentioned, which can be used for pumping aggressive fluids at high temperature, and yet works at low cost with high reliability, which is why in particular an entry of solid particles in the pulsator can be avoided should.
Diese Aufgabe wird durch eine Pumpenvorrichtung gemäß den Merkmalen des unabhängigen Anspruchs 1 gelöst. Vorteilhafte Ausgestaltungen der Erfindung sind in den abhängigen Ansprüchen angegeben. Erfindungsgemäß wird eine Pumpenvorrichtung mit einem Pulsator als Antriebselement für einen Hauptpumpenkopf, der in einer Förderleitung liegt und dessen Arbeitsraum mit einem saugseitigen Rückschlagventil und einem druckseitigen Rückschlagventil versehen ist, angegeben, wobei der Arbeitsraum des Pulsators über eine mit Fördermedium gefüllte Pendelleitung mit dem Arbeitsraum des Hauptpumpenkopfes in einer Weise in Verbindung steht, dass der Pulsator oszillierend Fördermedium aus der Förderleitung in den Arbeitsraum des Hauptpumpenkopfes ansaugt oder aus dem Arbeitsraum drückt, wobei ein Entlüftungsventil zur Entlüftung des Arbeitsraums des Pulsators vorgesehen ist, wobei das Entlüftungsventil ein zeitgesteuertes Ventil und/oder ein druckgesteuertes Doppelsitzventil ist und eine Vorrichtung zum Einleiten einer Flüssigkeit in den Arbeitsraum des Pulsators und/oder die Pendelleitung vorgesehen ist.This object is achieved by a pump device according to the features of
Die Verwendung eines zeitgesteuerten Ventils und/oder eines druckgesteuerten Doppelsitzventil hat den Vorteil, dass die Zeit, in der das Ventil zum Entlüften offen ist, sehr kurz gehalten werden kann, wodurch sich unerwünschte Nebenströme vermeiden lassen, die einen verstärkten Eintrag von Feststoffteilchen in den Pulsator zur Folge haben könnten.The use of a time-controlled valve and / or a pressure-controlled double-seat valve has the advantage that the time in which the valve is open for venting can be kept very short, as a result of which undesirable secondary flows can be avoided, which increase the entry of solid particles into the pulsator could result.
Das Einleiten von Flüssigkeit in den Arbeitsraum des Pulsators bzw. das Nachfüllen von Fördermedium in den Arbeitsraum zum Ausgleich von Verlusten beispielsweise durch das Entlüften des Arbeitsraums, hat den Vorteil, dass ein Flüssigkeitsausgleich nicht von dem getriebenen Hauptpumpenkopf erfolgen muss und somit keine Feststoffteilchen von dem Hauptpumpenkopf zu dem Pulsator transportiert werden. Vorzugsweise ist die Flüssigkeit Wasser und/oder Fördermedium und/oder eine andere geeignete Flüssigkeit.The introduction of liquid into the working area of the pulsator or the refilling of pumped medium into the working area to compensate for losses, for example by venting the working area, has the advantage that liquid balance does not have to take place from the driven main pump head and thus no solid particles from the main pump head to be transported to the pulsator. The liquid is preferably water and / or delivery medium and / or another suitable liquid.
Vorzugsweise umfasst die Vorrichtung zum Einleiten einer Flüssigkeit in den Arbeitsraum des Pulsators und/oder die Pendelleitung ein zeit- und/oder druckgesteuertes Nachfüllventil und/oder ein Nachfüllreservoir.The device for introducing a liquid into the work space of the pulsator and / or the pendulum line preferably comprises a time and / or pressure-controlled refill valve and / or a refill reservoir.
Vorzugsweise wird das zeit- und/oder druckgesteuerte Nachfüllventil bzw. Entlüftungsventil derart zeit- und/oder druckgesteuert, dass nach einer Anfahrphase des Prozesses das Nachfüllventil bzw. Entlüftungsventil geschlossen wird und/oder der obere Grenzwert zum Schließen des zeit- und/oder druckgesteuerten Nachfüllventils bzw. Entlüftungsventils nach einer Anfahrphase des Prozesses erhöht wird und/oder nach einer Anfahrphase des Prozesses der untere Grenzwert zum Schließen des zeit- und/oder druckgesteuerten Nachfüllventils bzw. Entlüftungsventils gesenkt wird.The time and / or pressure-controlled refill valve or vent valve is preferably time and / or pressure controlled such that after a start-up phase of the process the refill valve or vent valve is closed and / or the upper limit value for closing the time and / or pressure-controlled refill valve or vent valve is increased after a start-up phase of the process and / or after a start-up phase of the process the lower limit value for closing the time and / or pressure-controlled refill valve or vent valve is lowered.
Vorzugsweise entspricht der Druck, mit dem das Nachfüllreservoirs beaufschlagt wird, im Wesentlichen dem Druck in dem Arbeitsraum des Pulsators.The pressure which is applied to the refill reservoir preferably corresponds essentially to the pressure in the working space of the pulsator.
Vorzugsweise ist das Nachfüllventil zwischen dem Arbeitsraum und dem Nachfüllreservoir ein zeit- und/oder druckgesteuertes Ventil. Vorzugsweise ist der Arbeitsraum des Pulsators über das und/oder ein weiteres Entlüftungsventil mit der Saugseite der Förderleitung verbunden.The refill valve between the work space and the refill reservoir is preferably a time and / or pressure-controlled valve. The working space of the pulsator is preferably connected to the suction side of the delivery line via the and / or a further vent valve.
Vorzugsweise ist dabei vorteilhafterweise die Saugseite der Förderleitung zur selbsttätigen Entlüftung oberhalb des Entlüftungsventils angeordnet.Preferably, the suction side of the delivery line for automatic venting is advantageously arranged above the venting valve.
Alternativ oder zusätzlich ist vorzugsweise der Arbeitsraum des Pulsators über das und/oder ein weiteres Entlüftungsventil mit der Druckseite der Förderleitung verbunden.Alternatively or additionally, the working space of the pulsator is preferably connected to the pressure side of the delivery line via the and / or a further vent valve.
Vorzugsweise ist das Entlüftungsventil in Verbindung mit einer Rückführungspumpe zwangsgesteuert, insbesondere zeitlich gesteuert.The vent valve is preferably positively controlled in connection with a return pump, in particular timed.
Alternativ oder zusätzlich ist vorzugsweise der Arbeitsraum des Pulsators über das und/oder ein weiteres Entlüftungsventil mit einem Nachfüllreservoir zum Ausgleich von Leckageschwund in dem Arbeitsraum des Pulsators und/oder der Pendelleitung verbunden.Alternatively or additionally, the working area of the pulsator is preferably connected via the and / or a further vent valve to a refill reservoir to compensate for leakage shrinkage in the working area of the pulsator and / or the pendulum line.
Alternativ oder zusätzlich ist vorzugsweise der Arbeitsraum des Pulsators über das und/oder ein weiteres Entlüftungsventil mit einem Sammelbehälter zum Sammeln und zum eventuell späteren Rückführen von bei der Entlüftung austretendem Fördermedium verbunden.As an alternative or in addition, the working space of the pulsator is preferably connected via the and / or a further vent valve to a collecting container for collecting and for possibly returning the conveyed medium emerging during the venting.
Vorzugsweise ist das Ventil derart zeit- und/oder druckgesteuert, dass es zumindest oberhalb eines bestimmten Druckes geschlossen ist. Der Pulsator erzeugt im Arbeitsraum einen kontinuierlich abwechselnden Druck mit einer Druckphase und einer Saugphase. Um eine Abschwächung der Strömung aus der Pendelleitung zum Austreiben eventuell eingesaugter Feststoffpartikel zu verhindern, sollte zumindest ab einem bestimmten Druck im Arbeitsraum keine Entlüftung geschehen, um einen, wenn auch eventuell geringen, Druckabfall im Arbeitsraum und damit eine Verringerung der Strömung aus der Pendelleitung zu verhindern.The valve is preferably time and / or pressure controlled in such a way that it is closed at least above a certain pressure. The pulsator generates a continuously alternating pressure in the work area with a pressure phase and a suction phase. In order to prevent a weakening of the flow from the pendulum line to expel solid particles that may have been sucked in, at least a certain pressure in the work area should not be vented in order to prevent a pressure drop in the work area, albeit a small one, and thus a reduction in the flow from the pendulum line ,
Vorzugsweise ist das Ventil derart zeit- und/oder druckgesteuert, dass es zumindest unterhalb eines bestimmten Druckes geschlossen ist.The valve is preferably time and / or pressure controlled such that it is closed at least below a certain pressure.
Alternativ oder zusätzlich wird vorzugsweise eine Entlüftung unterhalb eines bestimmten Drucks im Arbeitsraum des Pulsators vermieden, denn durch den, wenn auch geringen Druckabfall würde eine größere Saugleistung und damit eine stärkere Strömung in die Pendelleitung auftreten, was mehr Feststoffpartikel in die Pendelleitung einsaugen könnte. Daher ist das Ventil vorzugsweise zumindest unterhalb eines bestimmten Druckes im Arbeitsraum geschlossen.As an alternative or in addition, venting below a certain pressure in the pulsator's working space is preferably avoided, because the, albeit small, pressure drop would result in greater suction power and thus a stronger flow into the pendulum line, which could suck more solid particles into the pendulum line. Therefore, the valve is preferably closed at least below a certain pressure in the work area.
Vorzugsweise erfolgt die Entlüftung nur in den zeitlichen Bereichen zwischen der Saug- und der Druckphase, wo eine im Wesentlichen geringe oder keine Strömung des Förderfluids in die Pendelleitung erfolgt. Dadurch kann die Strömung von Feststoff-Partikeln in die Pendelleitung verhindert werden.The venting preferably takes place only in the time ranges between the suction and the pressure phase, where there is essentially little or no flow of the delivery fluid into the pendulum line. This can prevent the flow of solid particles into the pendulum line.
Vorzugsweise weist die Pumpenvorrichtung ein Nachfüllreservoir zum Nachfüllen von Fördermedium auf, das mit einem Druck beaufschlagt ist, der im wesentlichen dem Systemdruck entspricht.The pump device preferably has a refill reservoir for refilling the conveyed medium, to which a pressure is applied which essentially corresponds to the system pressure.
Vorzugsweise ist bei allen Ausführungen der Erfindung die Pendelleitung mit einer Kühlung versehen.In all embodiments of the invention, the pendulum line is preferably provided with cooling.
Vorzugsweise ist bei allen Ausführungen der Erfindung der Pulsator oberhalb von dem Hauptpumpenkopf angeordnet. Zusätzlich oder alternativ ist vorzugsweise die Pendelleitung vom Pulsator zum Hauptpumpenkopf hin fallend ausgerichtet. Derartige Ausführungen der Erfindung haben den Vorteil, dass die Schwerkraft zusätzlich einem Eintrag von Feststoffpartikeln durch die Pendelleitung in den Pulsator entgegenwirkt.In all embodiments of the invention, the pulsator is preferably arranged above the main pump head. Additionally or alternatively, the pendulum line is preferably aligned falling from the pulsator to the main pump head. Such embodiments of the invention have the advantage that gravity additionally counteracts the entry of solid particles through the pendulum line into the pulsator.
Vorzugsweise ist die Pendelleitung mit einer Senke als Aufnahmeraum für Feststoffteilchen im Fördermedium versehen.The pendulum line is preferably provided with a depression as a receiving space for solid particles in the conveying medium.
Vorzugsweise ist der Arbeitsraum des Pulsators zumindest zeitweise mit einem Ausgleichsmedium zum Ausgleich von Leckageschwund beaufschlagt.The working space of the pulsator is preferably at least temporarily acted upon by a compensating medium to compensate for leakage shrinkage.
Vorzugsweise ist die Pendelleitung zumindest in einem Abschnitt in zumindest zwei parallele Teilabschnitte aufgeteilt.The pendulum line is preferably divided into at least one section into at least two parallel sections.
Vorzugsweise ist die Pendelleitung auch über ihren gesamten Verlauf geteilt, d.h. dass beispielsweise zwei oder mehr parallele Pendelleitungen vorgesehen sind.The pendulum line is preferably also divided over its entire course, i.e. that, for example, two or more parallel pendulum lines are provided.
Diese Ausführungen der Erfindung haben den Vorteil, dass durch Vorsehen einer entsprechenden Steuerung beispielsweise in der Saugphase die zumindest zwei Teilabschnitte geöffnet werden und in den Druckphasen zumindest ein Teilabschnitt (bei zwei Teilabschnitten vorzugsweise abwechselnd der eine und der andere Teilabschnitt) zumindest teilweise und vorzugsweise vollständig zumindest während eines Teil der Druckphase geschlossen wird, um durch die somit in dem bzw. den anderen Teilabschnitten resultierende höhere Ausströmgeschwindigkeit Ablagerungen von Feststoffteilchen in den Teilabschnitten zu verhindern.These embodiments of the invention have the advantage that by providing a corresponding control, for example in the suction phase, the at least two subsections are opened and in the printing phases at least one subsection (in the case of two subsections, preferably one and the other subsection alternately) at least partially and preferably completely at least is closed during part of the printing phase in order to prevent deposits of solid particles in the partial sections due to the higher outflow speed thus resulting in the other partial section (s).
Vorzugsweise ist das Volumen der parallel verlaufenden Teilabschnitte der Pendelleitung bzw. das Volumen der parallel verlaufenden Pendelleitungen jeweils zumindest so groß wie oder vorzugsweise größer als das Hubvolumen des Pulsators. Diese Weiterbildung der Erfindung hat den Vorteil, dass ein Austritt von Feststoffteilchen in die verbleibende Pendelleitung und/oder den Pulsator mit großer Wahrscheinlichkeit verhindert werden kann.The volume of the parallel sections of the pendulum line or the volume of the parallel pendulum lines is preferably at least as large as or preferably larger than the stroke volume of the pulsator. This development of the invention has the advantage that it is very likely that solid particles can escape into the remaining pendulum line and / or the pulsator.
Vorzugsweise sind können Steuerventile zum zumindest teilweisen Öffnen und Schließen der Teilabschnitte der Pendelleitung bzw. der parallelen Pendelleitungen vorgesehen.Control valves are preferably provided for at least partially opening and closing the sections of the pendulum line or the parallel pendulum lines.
Vorzugsweise wird eine Sensorik vorgesehen, um die zeitliche Steuerung der Steuerventile mit der jeweiligen Phasenlage der Pulsatormembran zu synchronisieren. Beispielsweise wird ein Sensor und/oder Schalter vorgesehen, der bei zumindest einer Endlage der Membran des Pulsators das Steuerventil schaltet. Alternativ oder zusätzlich wird ein Sensor und/oder Schalter für die andere Membranlage vorgesehen, um das Steuerventil zu schalten. Alternativ werden die Steuerventile auch nur während eines Teils der Druckphase in eine Schließstellung bzw. Teilschließstellung versetzt. Denkbar wäre auch während einer Druckphase nacheinander verschiedene Steuerventile zumindest teilweise zu schließen.A sensor system is preferably provided in order to synchronize the timing of the control valves with the respective phase position of the pulsator membrane. For example, a sensor and / or switch is provided which switches the control valve in at least one end position of the membrane of the pulsator. Alternatively or additionally, a sensor and / or switch is provided for the other membrane system in order to switch the control valve. Alternatively, the control valves are also put into a closed position or partially closed position only during part of the pressure phase. It would also be conceivable to at least partially close different control valves in succession during a printing phase.
Vorzugsweise ist die Pendelleitung vorzugsweise im Bereich vor dem Hauptpumpenkopf in mehrere parallel geschaltete Leitungen, vorzugsweise zwei parallel geschaltete Leitungen unterteilt, die zumindest teilweise und vorzugsweise vollständig durch ein zeit- und/oder druckgesteuertes Ventil zumindest teilweise verschließbar sind.The pendulum line is preferably divided in the area in front of the main pump head into a plurality of lines connected in parallel, preferably two lines connected in parallel, which are at least partially and preferably completely at least partially closable by a time and / or pressure-controlled valve.
Die Zeit- und/oder Drucksteuerung ist vorzugsweise derart eingestellt, dass während der Saugphase alle Leitungen möglichst lange offen sind, damit sich die Strömung auf die verschiedenen parallelen Leitungen verteilt, während in den Druckphasen abwechselnd eine Teilleitung mit dem vollen Druck und damit einer wesentlich höheren Strömungsgeschwindigkeit beaufschlagt wird. Dadurch sollte ein Eintrag von Feststoffteilchen in die Pendelleitung sicher vermieden werden.The time and / or pressure control is preferably set in such a way that all lines are open for as long as possible during the suction phase, so that the flow adjusts to the different ones in parallel Lines distributed, while in the pressure phases alternately a partial line with the full pressure and thus a much higher flow rate. As a result, the entry of solid particles into the pendulum line should be avoided.
Vorzugsweise weist der Hauptpumpenkopf zumindest zwei parallel geschaltete saugseitige Rückschlagventile auf.The main pump head preferably has at least two suction-side check valves connected in parallel.
Diese Ausführung der Erfindung hat den Vorteil, dass während der Druckphase in dem Leitungsabschnitt zwischen den Austritten der beiden saugseitigen Rückschlagventile eine höhere Strömungsgeschwindigkeit erzeugt wird, so dass die Gefahr des Eintritts von Feststoffteilchen in die Pendelleitung aus dem bezogen auf die Strömungsrichtung während der Druckphase stromabwärtigen saugseitige Rückschlagventil verringert wird.This embodiment of the invention has the advantage that a higher flow velocity is generated in the line section between the outlets of the two suction-side check valves during the pressure phase, so that the risk of solid particles entering the pendulum line from the suction side downstream of the flow direction during the pressure phase Check valve is reduced.
Vorzugsweise ist der Querschnitt der das bezogen auf die Strömungsrichtung während der Druckphase stromabwärtigen saugseitige Rückschlagventil aufnehmenden Leitung größer als der Querschnitt der das andere saugseitige Rückschlagventil aufnehmenden Leitung.The cross section of the line receiving the downstream suction-side check valve in relation to the flow direction during the pressure phase is preferably larger than the cross section of the line receiving the other suction-side check valve.
Das ist die bevorzugte Ausführung dieser bevorzugtenAusführungsform, denn dann werden mehr Feststoffteilchen durch die Leitung gefördert, die eine erhöhte Sicherheit gegenüber dem Eintrag von Feststoffteilchen in die Pendelleitung bietet. Alternativ könnten die Querschnitte der beiden Leitungen auch gleich groß sein oder mehr als zwei Leitungen und eine entsprechende Anzahl an saugseitigen Rückschlagventilen vorgesehen werden. Auch wäre ein größerer Querschnitt der das bezogen auf die Strömungsrichtung während der Druckphase stromaufwärtigen saugseitigen Rückschlagventil aufnehmenden Leitung denkbar, was immer noch einen wenn auch geringeren Vorteil gegenüber den Ausführungen mit nur einem saugseitigen Rückschlagventil bietet.This is the preferred embodiment of this preferred embodiment, because then more solid particles are conveyed through the line, which offers increased security against the entry of solid particles into the pendulum line. Alternatively, the cross sections of the two lines could also be the same size or more than two lines and a corresponding number of check valves on the suction side could be provided. It would also be conceivable to have a larger cross section of the line receiving upstream suction-side check valve in relation to the direction of flow during the pressure phase, which still offers an advantage, albeit a smaller one, than the designs with only one suction-side check valve.
Vorzugsweise ist in der Pendelleitung ein Trennkolben angeordnet.A separating piston is preferably arranged in the pendulum line.
Diese Ausführungen der Erfindung haben den Vorteil, dass der Trennkolben Feststoffteilchen daran hindert, durch die Pendelleitung von dem Hauptpumpenkopf zu dem Pulsator zu gelangen.These embodiments of the invention have the advantage that the separating piston prevents solid particles from passing through the pendulum line from the main pump head to the pulsator.
Vorzugsweise sind die genannten Ausführungen der erfindungsgemäßen Pumpenvorrichtung mit einem doppelt wirkenden Pulsator und zwei gegensinnig angesteuerten Pumpenkreisen ausgebildet.The above-mentioned embodiments of the pump device according to the invention are preferably designed with a double-acting pulsator and two pump circuits controlled in opposite directions.
Vorzugsweise ist der Pulsator als doppelt wirkender Pulsator ausgebildet ist, dessen eine Seite als Antriebselement für den Hauptpumpenkopf ausgebildet, und dessen andere Seite mit einem Druck beaufschlagt ist, der im Wesentlichen dem Systemdruck entspricht.The pulsator is preferably designed as a double-acting pulsator, one side of which is designed as a drive element for the main pump head, and the other side of which is acted upon by a pressure which essentially corresponds to the system pressure.
Derartige Ausführungen der Erfindung mit einem doppelt wirkenden Pulsator zum Antrieb von zwei gegenseitig angesteuerten Pumpenkreisen werden bevorzugt, denn dadurch kann eine gleichmäßige Förderung erreicht werden. Weiterhin kann der Pulsator bei hohen Saugdrücken von beispielsweise 250 bar mit einem für wesentlich geringere Drücke ausgelegten Antrieb angetrieben werden, wenn beispielsweise ein doppelt wirkender Kolben verwendet wird, der nur den Differenzdruck zwischen dem Druck während der Druckphase in der einen Pulsatorhälfte und dem Druck während der Saugphase in der jeweils anderen Pulsatorhälfte überwinden muss. Dieser Vorteil gilt auch für doppelt wirkende Pulsatoren zum Antrieb von nur einem Pumpenkreis, wenn die andere Seite des Pulsators, die nicht den Pumpenkreis antreibt, mit Druck beaufschlagt wird. Vorteilhafterweise ist dann bei Ausführungen der Erfindung mit einem Nachfüllreservoir für den bzw. die Membransteuerräume des Pulsators, das Nachfüllreservoir mit einem Druck beaufschlagt, der ungefähr dem Systemdruck entspricht, damit der Antrieb auch beim Nachfüllvorgang, der ventilgesteuert stattfindet, wenn die Membran ihre hintere mechanische Anlage erreicht, nicht einem höheren Druck als dem Differenzdruck zwischen Saug- und Druckphase ausgesetzt wird und somit nicht größer dimensioniert werden muss, und die Membran auch nicht an den Anströmkanälen ihrer hinteren mechanischen Anlage zerstört wird.Such embodiments of the invention with a double-acting pulsator for driving two mutually controlled pump circuits are preferred, since this enables uniform delivery. Furthermore, the pulsator can be driven at high suction pressures of, for example, 250 bar with a drive designed for significantly lower pressures, for example if a double-acting piston is used, which only the differential pressure between the pressure during the pressure phase in one half of the pulsator and the pressure during the Must overcome suction phase in the other half of the pulsator. This advantage also applies to double-acting pulsators for driving only one pump circuit when pressure is applied to the other side of the pulsator, which does not drive the pump circuit. Advantageously, in embodiments of the invention with a refill reservoir for the membrane control chamber or pulsators, the refill reservoir is pressurized with a pressure that approximately corresponds to the system pressure, so that the drive also takes place during the refill process, which is valve-controlled when the membrane is its rear mechanical system achieved, is not exposed to a higher pressure than the differential pressure between the suction and pressure phases and therefore does not have to be dimensioned larger, and the membrane is not destroyed at the flow channels of its rear mechanical system.
Vorzugsweise kann in dem Pulsator eine membranlagengesteuerte Nachfüll- und/oder Entlüftungsvorrichtung für Hydraulikflüssigkeit vorgesehen werden, wie sie beispielsweise aus der
Vorzugsweise ist Ausgleichsmedium zum Ausgleich von Leckageschwund in dem Membransteuerraum in einem Nachfüllreservoir vorhanden, das über ein Ventil mit dem Membransteuerraum verbunden ist, wobei das Nachfüllreservoir mit einem Druck beaufschlagt ist, der höher als der Atmosphärendruck ist.Compensating medium for compensating for leakage shrinkage is preferably present in the diaphragm control chamber in a refill reservoir which is connected to the diaphragm control chamber via a valve, the refill reservoir being pressurized to a pressure which is higher than atmospheric pressure.
Diese Ausführung der Erfindung hat den Vorteil, dass der Pulsator mit einem Antrieb (z.B. hydraulisch, mechanisch und/oder pneumatisch, z.B. ein Kolbentrieb) angetrieben werden kann, dessen Leistung nur den Druckunterschied zwischen der Saug- und der Druckseite überwinden muss. Außerdem kann durch eine Druckbeaufschlagung des Nachfüllreservoirs für den Leckageschwundausgleich im Membransteuerraum ein Stoß auf den Antrieb, beispielsweise den Kolben verhindert werden. Vorteilhafterweise kann dieser Druck im Nachfüllreservoir etwa dem Systemdruck entsprechen. Gemäß einer weiteren vorteilhaften Ausgestaltung der Erfindung wird eine mittels Regelkreis dem Systemdruck angepasste Druckregelung im Nachfüllreservoir vorgesehen, wie es beispielsweise in der
Vorzugsweise ist der Pulsator in Membran- oder Schlauchmembranbauweise ausgeführt.The pulsator is preferably constructed in the form of a membrane or tubular membrane.
Vorzugsweise ist der Pulsator in Kolben- oder Plungerbauweise ausgeführt.The pulsator is preferably designed in a piston or plunger construction.
Ein Grundgedanke der Erfindung liegt somit auch darin, dass der Pulsator einen Hauptpumpenkopf beaufschlagt, der prinzipiell wie ein Kolbenpumpenkopf ausgebildet ist, ohne dass jedoch ein Kolben erforderlich ist. Auf diese Weise kann als Pumpenkopf ein für hohe Temperaturen und Drücke geeignetes Standardbauteil verwendet werden, welches durch die Kombination mit einem Standard-Membranpulsator insgesamt eine kostengünstige Alternative zu den bekannten Lösungen darstellt, wobei das Prinzip einer "Remote Head"-Pumpe beibehalten wird. Der Verschleiß wird ferner dadurch verringert, dass eventuell im Fördermedium vorhandene Partikel nicht mit dem Arbeitsraum des Pulsators in Berührung kommen, da die Flüssigkeit in der Pendelleitung nur im Umfang des Pumpenhubs hin und her bewegt wird, und sich nur geringfügig mit frisch angesaugter Flüssigkeit mischt. Der Pulsator kann in Membran- oder Schlauchmembranbauweise sowie in Kolben- oder Plungerbauweise ausgeführt sein. Wenn es sich bei dem Pulsator um einen Membranpulsator handelt, gelangen Partikel nicht zur Membran. Da auch hohe Temperaturen im Fördermedium im Verlauf der Pendelleitung abnehmen, können Membranpulsatoren mit kostengünstigen KunststoffMembranen, beispielsweise aus PTFE, auch bei hohen Drücken und hohen Temperaturen in der Förderleitung eingesetzt werden. Daher sind erfindungsgemäße Pumpenvorrichtungen besonders gut zum Fördern von Biomasse bei der Herstellung von Biokraftstoff geeignet.A basic idea of the invention is therefore that the pulsator acts on a main pump head, which is basically designed like a piston pump head, but without the need for a piston. In this way, a standard component that is suitable for high temperatures and pressures can be used as the pump head, which, combined with a standard membrane pulsator, is an inexpensive alternative to the known solutions, while maintaining the principle of a "remote head" pump. The wear is further reduced by the fact that any particles present in the pumped medium do not come into contact with the working area of the pulsator, since the liquid in the pendulum line is only moved back and forth in the circumference of the pump stroke and mixes only slightly with freshly drawn-in liquid. The pulsator can be constructed in membrane or tubular membrane construction as well as in piston or plunger construction. If the pulsator is a membrane pulsator, particles do not get to the membrane. Since high temperatures in the pumped medium also decrease in the course of the pendulum line, membrane pulsators with inexpensive plastic membranes, for example made of PTFE, can also be used in the delivery line at high pressures and high temperatures. Pump devices according to the invention are therefore particularly well suited for conveying biomass in the production of biofuel.
Ein weiterer Vorteil liegt darin, dass sich aufgrund der Entlüftung Gase aus dem Fördermedium oder Lufteinschlüsse nicht in dem Pumpenraum des Pulsators ansammeln können, sondern in den Prozess zurück geführt werden. Bevorzugt liegt der Eintritt in die saugseitige Förderleitung zu diesem Zweck oberhalb des Entlüftungsventils, so dass die Gase selbsttätig aus dem Arbeitsraum austreten. Alternativ kann eine Zwangsentlüftung, beispielsweise mit einem zeit- und/oder druckgesteuerten Ventil vorhanden sein.Another advantage is that, due to the ventilation, gases from the pumped medium or air inclusions cannot accumulate in the pump room of the pulsator, but are returned to the process. For this purpose, the entry into the suction-side delivery line is preferably above the ventilation valve, so that the gases exit the working area automatically. Alternatively, there may be a forced ventilation, for example with a time and / or pressure controlled valve.
Um den Membranpulsator noch weiter temperaturmäßig zu entlasten, besteht eine bevorzugte Weiterbildung der Erfindung darin, dass die Pendelleitung mit einer Kühlung versehen ist.In order to further relieve the temperature of the membrane pulsator, a preferred development of the invention is that the pendulum line is provided with cooling.
Es erweist sich ferner als vorteilhaft, dass die Pendelleitung von dem Membranpulsator zum Hauptpumpenkopf hin fallend ausgerichtet ist. Die Partikel verbleiben somit im Bereich des Hauptpumpenkopfes und werden in die Förderleitung zurückgeführt.It also proves to be advantageous that the pendulum line is aligned to fall from the membrane pulsator to the main pump head. The particles thus remain in the area of the main pump head and are returned to the delivery line.
Alternativ kann es vorteilhaft sein, dass die Pendelleitung mit einer Senke als Aufnahmeraum für Feststoffteilchen im Fördermedium versehen ist. Es wird also in der Pendelleitung ein Bereich vorgesehen, der unterhalb des Arbeitsraums des Membranpulsators liegt, so dass die Partikel sich aufgrund der Schwerkraft dort ansammeln und nicht in den Arbeitsraum des Pulsators gelangen.Alternatively, it can be advantageous for the pendulum line to be provided with a depression as a receiving space for solid particles in the conveying medium. An area is therefore provided in the pendulum line which lies below the working space of the membrane pulsator, so that the particles collect there due to gravity and do not get into the working space of the pulsator.
Es ist zweckmäßig, dass der Arbeitsraum des Pulsators mit einem Ausgleichsmedium zum Ausgleich von Leckageschwund beaufschlagt ist, so dass ein Durchströmen der Pendelleitung und ein Wandern von Feststoffteilchen zum Pulsator verhindert werden.It is expedient that the working space of the pulsator is acted upon by a compensating medium to compensate for leakage shrinkage, so that flow through the pendulum line and migration of solid particles to the pulsator are prevented.
Um den Pulsator noch weiter gegen Feststoffteilchen aus dem Fördermedium zu schützen, besteht eine weitere vorteilhafte Ausgestaltung der Erfindung darin, in der Pendelleitung einen Trennkolben anzuordnen. Durch diese Maßnahme wird der dem Pulsator zugeordnete Teil der Pendelleitung von dem Teil getrennt, welcher dem Hauptpumpenkopf zugeordnet ist.In order to further protect the pulsator against solid particles from the pumped medium, a further advantageous embodiment of the invention consists in arranging a separating piston in the pendulum line. This measure separates the part of the pendulum line assigned to the pulsator from the part assigned to the main pump head.
Eine geringe Antriebsleistung wird dadurch erreicht, dass ein doppelt wirkender Pulsator und zwei gegensinnig angesteuerte Pumpenkreise vorhanden sind, was besonders beim Einsatz bei Rezirkulationsprozessen mit hohen Saugdrücken vorteilhaft ist.A low drive power is achieved in that there is a double-acting pulsator and two counter-driven pump circuits, which is particularly advantageous when used in recirculation processes with high suction pressures.
Nachfolgend wird die Erfindung anhand von Ausführungsbeispielen weiter erläutert. Es zeigen schematisch:
- Fig. 1
- einen Vertikalschnitt durch eine erste Ausführung einer Pumpenvorrichtung;
- Fig. 1A
- einen der
Fig. 1 entsprechenden Vertikalschnitt durch eine weitere erfindungsgemäße Pumpenvorrichtung mit einem doppelt wirkenden Pulsator und zwei gegensinnig angesteuerten Pumpenkreisen.Fig. 2 ein Schaltbild einer aus zwei Pumpenvorrichtungen nachFig. 1 zusammengesetzten Pumpenkonfiguration gemäß der Erfindung; - Fig. 3
- Merkmale weiterer Ausführungen einer erfindungsgemäßen Pumpenvorrichtung .
- Fig. 4
- ein
Fig. 2 entsprechendes Schaltbild einer alternativen erfindungsgemäßen Pumpenkonfiguration; - Fig. 5
- ein
Fig. 2 entsprechendes Schaltbild einer weiteren alternativen erfindungsgemäßen Pumpenkonfiguration; - Fig. 6
- ein
Fig. 2 entsprechendes Schaltbild einer weiteren alternativen erfindungsgemäßen Pumpenkonfiguration; - Fig. 7
- ein
Fig. 2 entsprechendes Schaltbild einer weiteren alternativen erfindungsgemäßen Pumpenkonfiguration; - Fig. 8
- Merkmale weiterer Ausführungen einer erfindungsgemäßen Pumpenvorrichtung .
- Fig. 9
- Merkmale weiterer Ausführungen einer erfindungsgemäßen Pumpenvorrichtung .
- Fig. 10
- ein Schaltbild einer aus zwei Pumpenvorrichtungen nach
Fig. 1 zusammengesetzten Pumpenkonfiguration gemäß der Erfindung; - Fig. 11
- ein p-V-Diagramm des zeitlichen Verlaufs des Drucks der Pumpe über dem Hubvolumen mit einer Angabe einer möglichen Nachfüllung während der Druckphase.
- Fig. 12
- ein p-V-Diagramm des zeitlichen Verlaufs des Drucks der Pumpe über dem Hubvolumen mit einer Angabe einer möglichen Nachfüllung während der Saugphase.
- Fig. 1
- a vertical section through a first embodiment of a pump device;
- Fig. 1A
- one of the
Fig. 1 corresponding vertical section through a further pump device according to the invention with a double-acting pulsator and two pump circuits driven in opposite directions.Fig. 2 a circuit diagram of one of two pump devicesFig. 1 composite pump configuration according to the invention; - Fig. 3
- Features of further designs of a pump device according to the invention.
- Fig. 4
- on
Fig. 2 corresponding circuit diagram of an alternative pump configuration according to the invention; - Fig. 5
- on
Fig. 2 corresponding circuit diagram of a further alternative pump configuration according to the invention; - Fig. 6
- on
Fig. 2 corresponding circuit diagram of a further alternative pump configuration according to the invention; - Fig. 7
- on
Fig. 2 corresponding circuit diagram of a further alternative pump configuration according to the invention; - Fig. 8
- Features of further designs of a pump device according to the invention.
- Fig. 9
- Features of further designs of a pump device according to the invention.
- Fig. 10
- a circuit diagram of one of two pump devices
Fig. 1 composite pump configuration according to the invention; - Fig. 11
- a pV diagram of the time course of the pressure of the pump over the stroke volume with an indication of a possible refill during the pressure phase.
- Fig. 12
- a pV diagram of the time course of the pressure of the pump over the stroke volume with an indication of a possible refill during the suction phase.
In der Beschreibung der Ausführungsbeispiele werden folgende Bezugszeichen verwendet:
- 1
- Pumpenvorrichtung
- 4
- Anschluss (für ein Nachfüllreservoir)
- 5
- Druckseite (der Förderleitung)
- 6
- Förderrichtung
- 7
- Anschluss (für die Pendelleitung)
- 8
- Anschluss (für eine Entlüftung)
- 9
- Entlüftungsventil
- 10
- Membranpulsator
- 11
- Hauptpumpenkopf
- 12
- Pendelleitung
- 12'
- Pendelleitung
- 121
- Teilabschnitt der Pendelleitung
- 122
- Teilabschnitt der Pendelleitung (parallel
geschaltet zu Teilabschnitt 121 der Pendelleitung) - 123
- Steuerventil (vorzugsweise ein druck- oder zeitgesteuertes Absperrventil)
- 124
- Steuerventil (vorzugsweise ein druck- oder zeitgesteuertes Absperrventil)
- 13
- Eingang
- 14
- Ausgang
- 15
- Saugseite (der Förderleitung)
- 16
- saugseitiges Rückschlagventil
- 161
- saugseitiges Rückschlagventil (parallel geschaltet zu saugseitigem Rückschlagventil 16)
- 17
- druckseitiges Rückschlagventil
- 18
- Arbeitsraum (des Hauptpumpenkopfes)
- 20
- Arbeitsraum (der Membranpulsator)
- 21
- Förderflüssigkeit
- 22
- Steuereingang (des Hauptpumpenkopfes)
- 23
- Kühlmantel
- 24
- Feststoffteilchen
- 25
- Abschnitt (in der Pendelleitung)
- 26
- Membran
- 27
- Membransteuerraum
- 28
- Kolben
- 281
- Scheibe
- 29
- Motor
- 30
- Nachfüllreservoir
- 31
- Ventil
- 32
- Trennkolben
- 33
- Bereich (auf Seite des Hauptpumpenkopfes)
- 34
- Bereich (auf Seite des Membranpulsators)
- 35
- Verschieberichtung Trennkolben
- 36
- Sammelbehälter
- 37
- Nachfüllventil des Membransteuerraums
- 38
- Hydraulikpumpe
- 39
- Entlüftungsventil des Membransteuerraums
- 1
- pump device
- 4
- Connection (for a refill reservoir)
- 5
- Discharge side (of the delivery line)
- 6
- conveying direction
- 7
- Connection (for the pendulum line)
- 8th
- Connection (for a vent)
- 9
- vent valve
- 10
- Membranpulsator
- 11
- Main pump head
- 12
- compensation line
- 12 '
- compensation line
- 121
- Section of the pendulum line
- 122
- Section of the pendulum line (connected in parallel to
section 121 of the pendulum line) - 123
- Control valve (preferably a pressure or time controlled shut-off valve)
- 124
- Control valve (preferably a pressure or time controlled shut-off valve)
- 13
- entrance
- 14
- output
- 15
- Suction side (of the delivery line)
- 16
- Check valve on the suction side
- 161
- Check valve on the suction side (connected in parallel to check
valve 16 on the suction side) - 17
- check valve on the pressure side
- 18
- Working area (of the main pump head)
- 20
- Working area (the membrane pulsator)
- 21
- pumped liquid
- 22
- Control input (of the main pump head)
- 23
- cooling jacket
- 24
- solid
- 25
- Section (in the pendulum line)
- 26
- membrane
- 27
- Diaphragm control chamber
- 28
- piston
- 281
- disc
- 29
- engine
- 30
- backfill
- 31
- Valve
- 32
- separating piston
- 33
- Range (on the main pump head side)
- 34
- Area (on the side of the membrane pulsator)
- 35
- Separation piston displacement direction
- 36
- Clippings
- 37
- Refill valve of the diaphragm control room
- 38
- hydraulic pump
- 39
- Bleed valve of the diaphragm control room
Gemäß
Die Pendelleitung 12 ist mit Förderflüssigkeit 21 gefüllt. Sie führt über einen Steuereingang 22 des Hauptpumpenkopfes 11 zum Arbeitsraum 20 des Membranpulsators 10. Die Pendelleitung 12 ist mit einer Kühlung versehen, die von einem mit Kühlflüssigkeit beaufschlagten Kühlmantel 23 gebildet wird. Auf diese Weise kann eine Temperaturabsenkung von beispielsweise ca. 360 <0>C am Hauptpumpenkopf 11, wie sie typischerweise die zu fördernde Bio-Masse bei der Bio-Kraftstoffherstellung aufweist, auf ca. 100 <0>C an dem Membranpulsator 10 vorgenommen werden.The
Da die Pendelleitung 12 die Förderflüssigkeit 21 enthält, welche auch Feststoffteilchen 24 aufweisen kann, ist ein Abschnitt 25 in der Pendelleitung 12 vorhanden, der von dem Membranpulsator 10 zum Hauptpumpenkopf 11 hin abfällt, und der unmittelbar in den Arbeitsraum 18 des Hauptpumpenkopfes 11 mündet. An ihrer tiefsten Stelle liegt die Pendelleitung 12 somit auf dem Niveau des Arbeitsraums 18 des Hauptpumpenkopfes 11. Die Feststoffteilchen 24 verbleiben dadurch aufgrund der Schwerkraft im Arbeitsraum 18 des Hauptpumpenkopfes 11 und gelangen nicht in den Arbeitsraum 20 des Membranpulsators 10. Sie werden vielmehr der druckseitigen Förderleitung 5 zugeführt. Der Membranpulsator 10 weist eine Membran 26 auf, die hydraulisch über einen Membransteuerraum 27 angesteuert wird. Als Membranwerkstoff eignet sich vorzugsweise PTFE. Alternativ können auch Elastomere, metallische Werkstoffe oder Verbundwerkstoffe eingesetzt werden. Der Membransteuerraum 27 wird mit einem Kolben 28 beaufschlagt, der mechanisch, z.B. von einem Motor 29 (
Unter Bezugnahme auf die
Wird der Kolben 28 ausgefahren, bewirkt dies ein Abflachen der Membran 26 und einen Unterdruck im Arbeitsraum 20 des Membranpulsators 10. Der Unterdruck wirkt über die Pendelleitung 12 im Arbeitsraum 18 des Hauptpumpenkopfes 11, so dass das saugseitige Rückschlagventil 16 öffnet und Förderflüssigkeit 21 von der Saugseite 15 der Förderleitung angesaugt wird. Beim folgenden entgegengesetzten Hub des Kolbens 28 wird beim Ausbauchen der Membran 26 Druck im Arbeitsraum 20 des Membranpulsators 10 erzeugt, der über die Pendelleitung 12 auf den Arbeitsraum 18 des Hauptpumpenkopfes 11 wirkt. Der Druck bewirkt ein Schließen des saugseitigen Rückschlagventils 16 und ein Öffnen des druckseitigen Rückschlagventils 17, so dass Förderflüssigkeit 21 in die Druckseite 5 der Förderleitung gepumpt wird. Durch oszillierende Bewegung des Kolbens 28 erfolgt auf diese Weise eine kontinuierliche Förderung.If the
Durch die gegensinnige Ansteuerung zweier Hauptpumpenköpfe 11 mittels doppelt wirkendem Pulsator 10, der vorzugsweise in Membranbauart ausgeführt ist, überlagern sich die Pump- und Saugvorgänge mit den zwei Kreisen A und B derart, dass insbesondere bei Rezirkulationsprozessen mit hohem Systemdruck und relativ niedrigem Differenzdruck zwischen Saug- und Druckleitung nur eine geringe Leistung für den Antrieb erforderlich ist. Alternativ kann jeder Hauptpumpenkopf 11 mit einem einfach wirkenden Pulsator gleich- oder gegensinnig angesteuert werden.Due to the opposite control of two main pump heads 11 by means of a double-acting
In
Die in den
Bei der Ausführungsform von
Die Pendelleitung 12 weist ein Gefälle hin zu den saugseitigen Rückschlagventilen 161, 16 auf. Beim Ansaugen verteilt sich der Saugstrom entsprechend der
Querschnittsverhältnisse auf die saugseitigen Rückschlagventile 161 und 16. Dadurch wird beim Saugen erreicht, dass im Pendelleitungsabschnitt zwischen diesen beiden saugseitigen Rückschlagventilen eine geringere Strömung stattfindet, als sie wäre, wenn die gesamte Ansaugmenge nur durch das saugseitige Rückschlagventil 16 angesaugt würde.The
Cross-sectional conditions on the suction-
Im Druckhub fließt durch die Pendelleitung die gesamteIn the pressure stroke, the entire flows through the pendulum line
Fördermenge der Pumpe. Dies führt dazu, dass man eine Strömung durch die Pendelleitung erhält, die in der Summe stärker zum saugseitigen Rückschlagventil 16 gerichtet ist.Flow rate of the pump. This leads to the fact that a flow is obtained through the pendulum line, which in total is directed more towards the suction-
Diese Strömung könnte dafür sorgen, dass die Ablagerungen vom Hauptstrom eher immer wieder zurückgefördert werden.This flow could ensure that the deposits from the main flow tend to be pumped back again and again.
Das Füllvolumen eines jeden Teilabschnitts 121, 122 sollte vorzugsweise mindestens genauso groß wie und vorzugsweise größer als das Hubvolumen des Pulsators sein. Dadurch wird verhindert, dass Feststoffpartikel durch das wechselweise Verschließen in der Druckphase hinter die steuernden Ventile gelangen.The filling volume of each
Bei einem ersten Saugvorgang würde so jeder Teilabschnitt zunächst maximal bis zur Hälfte seines Volumens mit Partikeln gefüllt. Der anschließend verschlossene Teilabschnitt würde diesen Zustand möglicherweise behalten. Beim erneuten Saugvorgang würde der Teilabschnitt dann maximal komplett mit Partikeln gefüllt sein, bevor in der Druckphase eine vollständige Ausspülung erfolgen würde.In a first suction process, each section would initially be filled with particles up to a maximum of half of its volume. The subsequently closed section would possibly keep this state. During the renewed suction process, the partial section would then be completely filled with particles at most, before a complete rinsing out would take place in the printing phase.
Bei der in
Die Pumpenvorrichtung von
Die
Die gestrichelte Linie in
Claims (18)
- Pump device (1) with a pulsator as drive element for a main pump head (11) which lies in a supply line (15) and the working space (18) of which is provided with a check valve (16) on the suction side and a check valve (17) on the pressure side, wherein the working space (20) of the pulsator is connected to the working space (18) of the main pump head (11) via a pendulum line (12) filled with supply medium (21), in such a way that the pulsator draws supply medium (21) oscillatingly from the conveying line (15) into the working space (18) of the main pump head (11) or presses it out of the working space (18), wherein a venting valve (9) is provided for venting the working space (20) of the pulsator, characterised in that the venting valve (9) is a time-controlled valve and/or a pressure-controlled double-seat valve and in that a device is provided for introducing a liquid into the working space of the pulsator and/or the pendulum line (12).
- Pump device (1) according to claim 1, characterised in that the working space (20) of the pulsator is connected to the suction side (15) of the supply line via the and/or a further vent valve (9).
- Pump device (1) according to one of the preceding claims, characterised in that the working space (20) of the pulsator is connected to the pressure side (5) of the supply line via the and/or a further vent valve (9).
- Pump device (1) according to one of the preceding claims, characterised in that the working space (20) of the pulsator is connected via the and/or a further vent valve (9) to a refill reservoir (30) for compensating for loss of leakage in the working space (20) of the pulsator and/or the pendulum line (12).
- Pump device (1) according to one of the preceding claims, characterised in that the working space (20) of the pulsator is connected via the and/or a further venting valve (9) to a collecting container (36) for collecting and possibly later returning supply medium (21) emerging during venting.
- Pump device (1) according to one of the preceding claims, characterised in that the pump device comprises a refill reservoir for refilling supply medium, which is subjected to a pressure which essentially corresponds to the system pressure.
- Pump device according to one of the preceding claims, characterised in that the pendulum line is provided with a cooling system.
- Pump device according to one of the preceding claims, characterised in that the pulsator is arranged above the main pump head.
- Pump device (1) according to one of the preceding claims, characterised in that the pendulum line (12) is divided at least in one section into at least two parallel partial sections (121, 122).
- Pump device (1) according to the preceding claim, characterised in that the volume of the parallel sub-sections (121, 122) of the pendulum line (12) or the volume of the parallel pendulum lines (121, 122) is in each case at least as large as or preferably greater than the stroke volume of the pulsator.
- Pump device (1) according to claim 9 or 10, characterised in that control valves (123, 124) are provided for at least partially opening and closing the partial sections (121, 122) of the pendulum line (12) or of the parallel pendulum lines.
- Pump device (1) according to one of the preceding claims, characterised in that the main pump head has at least two suction-side check valves (16, 161) arranged in parallel.
- Pump device (1) according to the preceding claim, characterised in that the cross-section of the line accommodating the downstream suction side check valve relative to the direction of flow during the pressure phase is larger than the cross-section of the line accommodating the other suction side check valve.
- Pump device (1) according to one of the preceding claims, characterised in that a separating piston (32) is arranged in the pendulum line (12').
- Pump device according to one of the preceding claims, characterised in that it is formed with a double-acting pulsator and two oppositely driven pump circuits (A, B).
- Pump device (1) according to one of the preceding claims, characterised in that the pulsator is designed as a double-acting pulsator, one side of which is designed as a driving element for the main pump head (11) and the other side of which is subjected to a pressure which corresponds substantially to the system pressure.
- Pump device according to one of the preceding claims, characterised in that the pulsator is of diaphragm or hose-diaphragm construction.
- Pump device according to one of the preceding claims 1 to 16, characterised in that the pulsator is of piston or plunger design.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL09777900T PL2329147T3 (en) | 2008-08-14 | 2009-08-14 | Pumping device |
EP09777900.3A EP2329147B1 (en) | 2008-08-14 | 2009-08-14 | Pumping device |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08014528.7A EP2154371B1 (en) | 2008-08-14 | 2008-08-14 | Pumping device |
EP09777900.3A EP2329147B1 (en) | 2008-08-14 | 2009-08-14 | Pumping device |
PCT/EP2009/005928 WO2010017997A2 (en) | 2008-08-14 | 2009-08-14 | Pump device |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2329147A2 EP2329147A2 (en) | 2011-06-08 |
EP2329147B1 true EP2329147B1 (en) | 2019-12-18 |
Family
ID=39883770
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
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EP08014528.7A Active EP2154371B1 (en) | 2008-08-14 | 2008-08-14 | Pumping device |
EP09777900.3A Active EP2329147B1 (en) | 2008-08-14 | 2009-08-14 | Pumping device |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
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EP08014528.7A Active EP2154371B1 (en) | 2008-08-14 | 2008-08-14 | Pumping device |
Country Status (8)
Country | Link |
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US (1) | US20110135514A1 (en) |
EP (2) | EP2154371B1 (en) |
CN (1) | CN102124226B (en) |
BR (1) | BRPI0917663A2 (en) |
DK (1) | DK200800165U3 (en) |
ES (1) | ES2773043T3 (en) |
PL (1) | PL2329147T3 (en) |
WO (1) | WO2010017997A2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2761180B1 (en) * | 2011-09-30 | 2018-11-21 | MHWirth GmbH | Positive displacement pump |
DE102012102088A1 (en) | 2012-03-13 | 2013-09-19 | Prominent Dosiertechnik Gmbh | Positive displacement pump with forced ventilation |
KR101374048B1 (en) * | 2012-06-14 | 2014-03-13 | 한국과학기술연구원 | Fluid pumping device, fuel cell device and fuel gas recirculation method using the same |
DE102013114320A1 (en) * | 2013-12-18 | 2015-06-18 | Mhwirth Gmbh | Hot sludge pump |
US11001550B2 (en) * | 2014-07-11 | 2021-05-11 | Ibj Technology Aps | Method and apparatus for producing biofuel in an oscillating flow production line under supercritical fluid conditions |
DE102016015110A1 (en) * | 2016-12-20 | 2018-06-21 | Fresenius Medical Care Deutschland Gmbh | Positive displacement pump for medical fluids and blood treatment device with a positive displacement pump for medical fluids and method for controlling a positive displacement pump for medical fluids |
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US2444586A (en) * | 1944-03-20 | 1948-07-06 | Wuensch Charles Erb | Pump |
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US3216360A (en) * | 1963-06-10 | 1965-11-09 | Lapp Insulator Company Inc | Fluid transport device |
GB1108423A (en) * | 1964-01-08 | 1968-04-03 | Panther Pumps & Equipment Comp | Method of transmitting power by means of a fluid medium |
US3661167A (en) * | 1970-05-25 | 1972-05-09 | A & D Fabricating Co | Chemical feed pump with improved valve means |
JPS5018604B1 (en) * | 1971-06-24 | 1975-07-01 | ||
US3802807A (en) * | 1972-06-02 | 1974-04-09 | Precision Control Prod Corp | Pump |
DE2553794A1 (en) * | 1975-11-29 | 1977-06-02 | Bayer Ag | Continuous delivery of hot aggressive fluids - uses sealing liquid arranged to produce temperature drop to safe level |
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DE3012028A1 (en) * | 1980-03-28 | 1981-10-08 | Josef Emmerich Pumpenfabrik GmbH, 5481 Hönningen | DEVICE FOR CONVEYING FLOWABLE MEDIA |
DE3021851C2 (en) * | 1980-06-11 | 1984-04-12 | Pumpenfabrik Urach, 7432 Urach | High pressure piston pump |
US4378183A (en) * | 1980-09-18 | 1983-03-29 | The Pittsburgh & Midway Coal Mining Co. | Apparatus and method for pumping hot, erosive slurry of coal solids in coal derived, water immiscible liquid |
US4386888A (en) * | 1980-09-29 | 1983-06-07 | Mccann's Engineering And Manufacturing Company | Double diaphragm operated reversing valve pump |
DE3040478C2 (en) * | 1980-10-28 | 1986-07-10 | Uraca Pumpenfabrik GmbH & Co KG, 7432 Bad Urach | Pump or the like. hydraulic working machine |
ATE10670T1 (en) * | 1980-12-29 | 1984-12-15 | Lewa Herbert Ott Gmbh + Co. | DIAPHRAGM PUMP WITH RELIEVED CLAMPED DIAPHRAGM. |
DE3261319D1 (en) * | 1982-02-05 | 1985-01-10 | Bran & Luebbe | Piston-driven diaphragm pump |
US5310321A (en) * | 1990-07-24 | 1994-05-10 | Baker Hughes Incorporated | Pump system |
US5249932A (en) * | 1991-10-07 | 1993-10-05 | Erik Van Bork | Apparatus for controlling diaphragm extension in a diaphragm metering pump |
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IT1297087B1 (en) | 1997-11-28 | 1999-08-03 | Enea Ente Nuove Tec | DEVICE FOR PUMPING LIQUIDS OR AERIFORMS, WITH DOUBLE ACTING ALTERNATIVE MOTION OBTAINED BY HYDRAULIC SYSTEM. |
DE19903061C2 (en) * | 1999-01-26 | 2002-11-21 | Emmerich Josef Pumpenfab | displacement |
US7175397B2 (en) * | 2002-09-27 | 2007-02-13 | Pulsafeeder, Inc. | Effervescent gas bleeder apparatus |
DE102006041420A1 (en) * | 2006-09-04 | 2008-03-20 | Bran + Luebbe Gmbh | pump device |
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2008
- 2008-08-14 EP EP08014528.7A patent/EP2154371B1/en active Active
- 2008-08-27 DK DK200800165U patent/DK200800165U3/en not_active IP Right Cessation
-
2009
- 2009-08-14 BR BRPI0917663A patent/BRPI0917663A2/en not_active Application Discontinuation
- 2009-08-14 US US13/058,904 patent/US20110135514A1/en not_active Abandoned
- 2009-08-14 EP EP09777900.3A patent/EP2329147B1/en active Active
- 2009-08-14 WO PCT/EP2009/005928 patent/WO2010017997A2/en active Application Filing
- 2009-08-14 CN CN200980131732.1A patent/CN102124226B/en active Active
- 2009-08-14 PL PL09777900T patent/PL2329147T3/en unknown
- 2009-08-14 ES ES09777900T patent/ES2773043T3/en active Active
Non-Patent Citations (1)
Title |
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None * |
Also Published As
Publication number | Publication date |
---|---|
EP2329147A2 (en) | 2011-06-08 |
WO2010017997A3 (en) | 2010-04-08 |
BRPI0917663A2 (en) | 2015-12-01 |
DK200800165U3 (en) | 2009-12-11 |
EP2154371A1 (en) | 2010-02-17 |
CN102124226B (en) | 2014-09-17 |
CN102124226A (en) | 2011-07-13 |
EP2154371B1 (en) | 2018-09-19 |
PL2329147T3 (en) | 2020-06-29 |
WO2010017997A2 (en) | 2010-02-18 |
US20110135514A1 (en) | 2011-06-09 |
ES2773043T3 (en) | 2020-07-09 |
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